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JP2005272760A - ε-type crystal copper phthalocyanine and process for producing the same - Google Patents

ε-type crystal copper phthalocyanine and process for producing the same Download PDF

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JP2005272760A
JP2005272760A JP2004091537A JP2004091537A JP2005272760A JP 2005272760 A JP2005272760 A JP 2005272760A JP 2004091537 A JP2004091537 A JP 2004091537A JP 2004091537 A JP2004091537 A JP 2004091537A JP 2005272760 A JP2005272760 A JP 2005272760A
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copper phthalocyanine
type crystal
type
acid
weight
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Osamu Jomaru
修 城丸
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Artience Co Ltd
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Toyo Ink Mfg Co Ltd
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Priority to JP2004091537A priority Critical patent/JP2005272760A/en
Priority to US11/086,364 priority patent/US7211664B2/en
Priority to EP05251852A priority patent/EP1580239A1/en
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Abstract

【課題】多大なエネルギーを必要とし、その上、設備負荷および環境負荷が大きなε型結晶形銅フタロシアニンの
製造法を改良すること。
【解決手段】アシッドペースティング法またはアシッドスラリー法によって得られるα型結晶単独またはε型結晶との混合物である銅フタロシアニンを、ヨウ素、臭素、キノン類等のルイス酸共存下、溶剤中80〜250℃で処理することによってε型結晶形銅フタロシアニンを製造する。
【選択図】なし
[PROBLEMS] To improve a method for producing an ε-type crystal copper phthalocyanine which requires a large amount of energy and has a large equipment load and environmental load.
Copper phthalocyanine, which is an α-type crystal alone or a mixture with an ε-type crystal obtained by an acid pasting method or an acid slurry method, is mixed in a solvent in the presence of a Lewis acid such as iodine, bromine and quinones in an amount of 80 to 250. Ε-type crystalline copper phthalocyanine is produced by treating at ℃.
[Selection figure] None

Description

本発明は、空気雰囲気下、昇温速度5℃・min−1での示差熱分析法による温度範囲425±25℃における発熱ピークが単一であるε型結晶形銅フタロシアニンおよびその製造法に関するものである。 TECHNICAL FIELD The present invention relates to an ε-type crystal copper phthalocyanine having a single exothermic peak in a temperature range of 425 ± 25 ° C. by differential thermal analysis at a heating rate of 5 ° C. · min −1 in an air atmosphere and a method for producing the same. It is.

ε型結晶形銅フタロシアニンはα型結晶と比較して色相赤味、高鮮明、高着色力であり、かつ、一次結晶の結晶成長に対する耐溶剤性がβ型結晶よりも大きく、さらにβ型への結晶転移に対する耐溶剤性が他の同質異晶銅フタロシアニンよりも大きいために、色相の変化ならびに着色力および鮮明性の低下の懸念が少ないという極めて優れた特性を有した結晶形の分子集合体である。さらに、ε型結晶の熱力学的安定性は同質異晶結晶中で最も安定な結晶形であるβ型の次に位置している。 ε-type crystal copper phthalocyanine has a red hue, high vividness, and high tinting strength compared to α-type crystals, and the solvent resistance to crystal growth of primary crystals is larger than β-type crystals. Crystalline molecular aggregates with extremely excellent characteristics that there is less concern of hue change and coloring power and sharpness reduction due to higher solvent resistance to crystal transition of other homogeneous heterogeneous copper phthalocyanines It is. Furthermore, the thermodynamic stability of the ε-type crystal is next to the β-type, which is the most stable crystal form among homogenous heterocrystalline crystals.

ε型結晶形銅フタロシアニンの代表的な製造法はε型およびβ型以外の結晶形の銅フタロシアニンを有機溶剤中で強い機械的力を掛けて長時間ミリングするソルベントソルトミリング法である(特許文献1参照)。
ε型結晶形への転移の制御を困難にさせている最大の要因はβ型と類似したその分子配列にあると考えられる。ε型結晶のCuKα粉末X線回折プロファイルで特徴的な回折角7.5°および9.0°のピークはそれぞれミラー指数001面および20面における反射に起因すること、およびβ型と類似した分子配列であることが結晶構造解析により推定された。従来の製造法における強い機械的力はポテンシャルエネルギーが最小であるβ型結晶形の分子配列を経由させない役割を担い、β型への転移を抑制すると考えられる。
特開昭48−76925号公報
A typical method for producing ε-type crystal copper phthalocyanine is a solvent salt milling method in which copper phthalocyanine having a crystal form other than ε-type and β-type is milled in an organic solvent for a long time by applying a strong mechanical force (Patent Document). 1).
The biggest factor that makes it difficult to control the transition to the ε-type crystal form is thought to be its molecular arrangement similar to the β-type. Peaks with diffraction angles of 7.5 ° and 9.0 ° characteristic of CuKα powder X-ray diffraction profile of ε-type crystals are attributed to reflection on Miller index 001 and 20 planes, respectively, and molecules similar to β-type The structure was estimated by crystal structure analysis. It is considered that the strong mechanical force in the conventional manufacturing method plays a role of not passing through the molecular arrangement of the β-type crystal form having the minimum potential energy and suppresses the transition to the β-type.
JP-A-48-76925

解決しようとする問題点は、ε型結晶形銅フタロシアニンの製造がエネルギーと時間の面からコストに大きく反映する強い機械的力を必要とすること、ならびに、摩砕助剤として使用される塩類やCOD値の高い高沸点溶剤を使用しなければならず、それらは設備や環境に対する負荷が大きいことである。 The problems to be solved are that the production of ε-type crystalline copper phthalocyanine requires a strong mechanical force that greatly reflects the cost from the viewpoint of energy and time, as well as the salts used as grinding aids, High boiling solvents with a high COD value must be used, which is a heavy load on equipment and the environment.

本発明は、空気雰囲気下、昇温速度5℃・min−1での示差熱分析法による温度範囲425±25℃における発熱ピークが単一であるε型結晶形銅フタロシアニンに関する。 The present invention relates to an ε-type crystalline copper phthalocyanine having a single exothermic peak in a temperature range of 425 ± 25 ° C. according to differential thermal analysis at a heating rate of 5 ° C. · min −1 in an air atmosphere.

更に本発明は、銅フタロシアニンをルイス酸共存下、溶剤中80〜250℃で処理することによって得られる上記ε型結晶形銅フタロシアニンの製造法に関する。     Furthermore, this invention relates to the manufacturing method of the said (epsilon) type crystal form copper phthalocyanine obtained by processing copper phthalocyanine in a solvent at 80-250 degreeC by coexistence of a Lewis acid.

更に本発明は、ルイス酸がヨウ素である上記製造法に関する。     Furthermore, the present invention relates to the above production method wherein the Lewis acid is iodine.

更に本発明は、ルイス酸が臭素である上記製造法に関する。     Furthermore, the present invention relates to the above production method, wherein the Lewis acid is bromine.

更に本発明は、ルイス酸がキノン類である上記製造法に関する。     Furthermore, this invention relates to the said manufacturing method whose Lewis acid is quinones.

更に本発明は、銅フタロシアニンがα型結晶単独またはε型結晶との混合物である上記製造法に関する。 Furthermore, the present invention relates to the above production method, wherein the copper phthalocyanine is an α-type crystal alone or a mixture with an ε-type crystal.

更に本発明は、銅フタロシアニンがアシッドペースティング法またはアシッドスラリー法によって得られるα型結晶単独またはε型結晶との混合物である上記製造法に関する。 Furthermore, the present invention relates to the above production method, wherein the copper phthalocyanine is an α-type crystal alone or a mixture with an ε-type crystal obtained by an acid pasting method or an acid slurry method.

銅フタロシアニンは色相、耐性、コスト等の点から有機顔料中で最も使用量が多く重要な藍色顔料である。その中でもε型結晶形銅フタロシアニンは極めて優れた用途適性を有した分子集合体である。その製造が従来のような強い機械的力無しに実現した結果、エネルギーならびに設備および環境に対する負荷を激減させ工業的に極めて有利に製造することが出来た。 Copper phthalocyanine is the most important indigo pigment among organic pigments in terms of hue, resistance and cost. Among them, the ε-type crystal form copper phthalocyanine is a molecular assembly having extremely excellent aptitude for use. As a result of the realization without the strong mechanical force as in the prior art, the load on energy and equipment and the environment can be drastically reduced and the production can be carried out extremely advantageously industrially.

本発明における銅フタロシアニンは銅フタロシアニンを5〜15重量倍の65〜100%硫酸に加え3〜8時間かき混ぜて硫酸塩または硫酸溶液とし30〜50重量倍の水中に注入して得られるか、または銅フタロシアニンを5〜15重量倍の65〜100%硫酸に加え3〜8時間かき混ぜて硫酸塩または硫酸溶液とし30〜50重量倍の水中に注入して微細α型結晶形銅フタロシアニンとして得られる。以上のように酸として一般的に硫酸が用いられ、濃度80数%以上の硫酸を用いた場合に銅フタロシアニンは高粘性溶液状態となることからアシッドペースティング法と呼ばれ、一方、60数%から80数%の硫酸を用いた場合に銅フタロシアニンはその硫酸塩が分散した状態となることからアシッドスラリー法と呼ばれている。 The copper phthalocyanine in the present invention can be obtained by adding copper phthalocyanine to 5 to 15 times by weight 65 to 100% sulfuric acid and stirring for 3 to 8 hours to give a sulfate or sulfuric acid solution and injecting it into 30 to 50 times by weight water, or Copper phthalocyanine is added to 65 to 100% sulfuric acid in an amount of 5 to 15 times by weight and stirred for 3 to 8 hours to obtain a sulfate or sulfuric acid solution, which is injected into 30 to 50 times by weight of water to obtain fine α-type crystal form copper phthalocyanine. As described above, sulfuric acid is generally used as an acid. When sulfuric acid having a concentration of 80% or more is used, copper phthalocyanine is called an acid pasting method because it is in a highly viscous solution state. When 80 to 80% sulfuric acid is used, copper phthalocyanine is called the acid slurry method because its sulfate is dispersed.

本発明における銅フタロシアニンの結晶形はα型結晶形だけではなく、ε型結晶形より大きなポテンシャルエネルギーの結晶形である例えばδやγ型結晶形でも構わないが、α型結晶形が容易に製造される点で有利である。 The crystal form of copper phthalocyanine in the present invention is not limited to the α-type crystal form, but may be a crystal form having a larger potential energy than the ε-type crystal form, for example, a δ or γ-type crystal form. Is advantageous.

本発明における溶剤はtert−ブチルベンゼン類やtert−アミルベンゼン類のような3級アルキルベンゼン類、ニトロベンゼン類、スルホランのような脂環族、またはこれらの混合物である。
本発明における処理温度は80〜250℃で、好ましくは120〜180℃である。80℃より温度が低いとα型からε型へ転移しない。250℃より温度が高いと一次結晶が成長し顔料として不利であり、かつ熱エネルギーの無駄になる。
The solvent in the present invention is a tertiary alkylbenzene such as tert-butylbenzene or tert-amylbenzene, an alicyclic group such as nitrobenzene or sulfolane, or a mixture thereof.
The processing temperature in this invention is 80-250 degreeC, Preferably it is 120-180 degreeC. If the temperature is lower than 80 ° C., the α type does not transition to the ε type. When the temperature is higher than 250 ° C., primary crystals grow, which is disadvantageous as a pigment and wastes heat energy.

本発明におけるルイス酸はヨウ素、臭素またはベンゾキノン、ナフトキノン、p−クロラニルのキノン類であり、ヨウ素、臭素が特に優れる。β型における銅フタロシアニン分子の中心金属銅原子の配位子場は分子内ピロール窒素原子4個と隣接銅フタロシアニン分子内メソ位窒素原子2個とから構成された八面体構造である。この構造がβ型の安定性の要因である。背景技術の項で言及した機械的力の作用は隣接銅フタロシアニン分子内メソ位窒素原子2個が銅原子へ軸配位するのを力学的に抑制しβ型結晶形への転移を阻止することであると考えられる。それに対し、ルイス酸は化学的に抑制する。メソ位窒素原子は銅フタロシアニン分子内でフロンティア電子密度が最大であり、それ故、酸や金属原子空軌道に対する配位能が高い。ルイス酸は銅フタロシアニンと電荷移動錯体を形成することによってメソ位窒素原子の電子密度を低下させ、銅原子への配位を抑制すると考えられる。本発明での使用量はフタロシアニン化合物全量に対しモル比0.01〜2.0であり、好ましくは、0.05〜0.5である。 The Lewis acid in the present invention is iodine, bromine, benzoquinone, naphthoquinone, p-chloranil quinones, and iodine and bromine are particularly excellent. The ligand field of the central metal copper atom of the copper phthalocyanine molecule in β-type is an octahedral structure composed of 4 pyrrole nitrogen atoms in the molecule and 2 meso-position nitrogen atoms in the adjacent copper phthalocyanine molecule. This structure is a factor of β-type stability. The action of the mechanical force referred to in the background section mechanically suppresses the axial coordination of two meso-position nitrogen atoms in the adjacent copper phthalocyanine molecule to the copper atom and prevents the transition to the β-type crystal form. It is thought that. In contrast, Lewis acids are chemically suppressed. The meso-position nitrogen atom has the highest frontier electron density in the copper phthalocyanine molecule, and therefore has high coordination ability for acid and metal vacancies. The Lewis acid is thought to reduce the electron density of the meso-position nitrogen atom by forming a charge transfer complex with copper phthalocyanine and suppress the coordination to the copper atom. The usage-amount in this invention is 0.01-2.0 molar ratio with respect to the phthalocyanine compound whole quantity, Preferably, it is 0.05-0.5.

なお、溶剤処理の際に、ε型結晶形銅フタロシアニンを種結晶として共存させておくのが好ましい。その理由は、種結晶は結晶核作用によって初期の転移速度を増大させる効果を有するからである。使用量は銅フタロシアニンとフタロシアニン誘導体との混合物全量に対して1/5〜1/10が適当である。 In the solvent treatment, it is preferable that ε-type crystal copper phthalocyanine coexists as a seed crystal. This is because the seed crystal has the effect of increasing the initial transition rate by the crystal nucleus action. The amount used is suitably 1/5 to 1/10 based on the total amount of the mixture of copper phthalocyanine and phthalocyanine derivative.

本発明によって得られたε型結晶形銅フタロシアニンのBET法による比表面積/m・g−1は60±5と大きな値であり、グラビアインキ、オフセットインキ、塗料、または着色樹脂等にそのまま顔料として使用出来る品質であった。本発明によって得られた溶剤処理スラリー、精製溶剤スラリーまたは粉体の形態のε型結晶形銅フタロシアニンを、引き続きフタロシアニン誘導体を共存させて、または共存させずにソルベントミリング法やソルベントソルトミリング法による顔料化を行うことによって着色力や鮮明性をより一層向上させることが出来、極めて高品質の顔料を容易に製造することが出来た。 Specific surface area / m 2 · g −1 of the ε-type crystal copper phthalocyanine obtained by the present invention by BET method is a large value of 60 ± 5, and it is a pigment as it is in gravure ink, offset ink, paint, or colored resin. It was quality that can be used as. Ε-type crystalline copper phthalocyanine in the form of solvent-treated slurry, purified solvent slurry or powder obtained by the present invention, and pigment by solvent milling method or solvent salt milling method with or without phthalocyanine derivative As a result, coloring power and sharpness could be further improved, and extremely high-quality pigments could be easily produced.

また、本発明によって得られた溶剤処理スラリー、精製溶剤スラリーまたは粉体の形態のε型結晶形銅フタロシアニンに界面活性剤を処理する、またはフタロシアニン誘導体をドライブレンドまたはスラリーブレンドすることによって、グラビアインキ、オフセットインキ、塗料、または着色樹脂等に使用した際に用途適性を持たせることが出来た。 Further, the gravure ink is obtained by treating the ε-type crystalline copper phthalocyanine in the form of a solvent-treated slurry, purified solvent slurry or powder obtained by the present invention with a surfactant, or by dry blending or slurry blending a phthalocyanine derivative. When used in offset inks, paints, colored resins, etc., application suitability could be given.

本発明によって得られたε型結晶形銅フタロシアニンはフタロシアニン誘導体を含まず、空気雰囲気下、昇温速度5℃・min−1での示差熱分析法による温度範囲425±25℃における発熱ピークが単一であった。この分析結果は銅フタロシアニン以外のフタロシアニン化合物が含まれないことを示し、本発明の製法によって初めて実現された。 The ε-type crystalline copper phthalocyanine obtained by the present invention does not contain a phthalocyanine derivative, and has a single exothermic peak in a temperature range of 425 ± 25 ° C. according to differential thermal analysis at a heating rate of 5 ° C./min −1 in an air atmosphere. It was one. This analysis result shows that no phthalocyanine compound other than copper phthalocyanine is contained, and was realized for the first time by the production method of the present invention.

(比較例)
粗製銅フタロシアニン73重量部とテトラクロロフタルイミドメチル化銅フタロシアニン(テトラクロロフタルイミドメチル基の置換数は1個/モル)7重量部とを500重量部の95%硫酸に加え3時間かき混ぜて硫酸溶液とし4Lの水中に注入した。濾過後、残渣を水洗、熱風乾燥し、得られたα型結晶形銅フタロシアニンを粉砕した。 次に、得られた銅フタロシアニンとフタロシアニン誘導体との混合物をε型結晶形銅フタロシアニン20重量部、粉砕食塩600重量部、ポリエチレングリコール100重量部と共にニーダ−に入れ、100〜140℃で10時間摩砕した。取り出し後、2%硫酸溶液で精製し、濾過、水洗、乾燥した。得られた顔料はε型結晶形であった。粉末X線回折プロファイルを図1に示した。また、空気雰囲気下、昇温速度5℃・min−1での示差熱分析法によるDTA曲線を図2に示した。
(Comparative example)
Add 73 parts by weight of crude copper phthalocyanine and 7 parts by weight of tetrachlorophthalimidomethylated copper phthalocyanine (the number of substitution of tetrachlorophthalimidomethyl group is 1 / mol) to 500 parts by weight of 95% sulfuric acid and stir for 3 hours to obtain a sulfuric acid solution. Injection into 4 L of water. After filtration, the residue was washed with water and dried with hot air, and the α-type crystalline copper phthalocyanine obtained was pulverized. Next, the obtained mixture of copper phthalocyanine and phthalocyanine derivative was put in a kneader together with 20 parts by weight of ε-type crystalline copper phthalocyanine, 600 parts by weight of pulverized sodium chloride, and 100 parts by weight of polyethylene glycol, and the mixture was polished at 100 to 140 ° C. for 10 hours. Crushed. After removal, the mixture was purified with a 2% sulfuric acid solution, filtered, washed with water, and dried. The obtained pigment was in the ε-type crystal form. The powder X-ray diffraction profile is shown in FIG. In addition, FIG. 2 shows a DTA curve obtained by differential thermal analysis at a temperature rising rate of 5 ° C. · min −1 in an air atmosphere.

粗製銅フタロシアニン85重量部を500重量部の98%硫酸に加え3時間かき混ぜて硫酸溶液とし4Lの水中にアスピレ−タを通して注入した。濾過後、残渣を水洗、熱風乾燥し、得られたα型結晶形銅フタロシアニンを粉砕した。 次に、得られた微細α型結晶形銅フタロシアニンをε型結晶形銅フタロシアニン15重量部およびヨウ素4重量部と共に、スルホラン1000重量部中、170℃、6時間加熱撹拌した。室温付近まで冷却後、メタノール1000重量部中へ注入し、濾過後、残渣をメタノール洗、熱風乾燥した。粉末X線回折分析法でα型およびβ型を全く含まないε型結晶形銅フタロシアニンが定量的に得られた。粉末X線回折プロファイルを図3に示した。また、空気雰囲気下、昇温速度5℃・min−1での示差熱分析法によるDTA曲線を図4に示した。温度範囲425±25℃における発熱ピークが比較例では2本であるのに対して実施例1は単一であり、誘導体の有無による差異が明らかである。 85 parts by weight of crude copper phthalocyanine was added to 500 parts by weight of 98% sulfuric acid and stirred for 3 hours to obtain a sulfuric acid solution, which was poured into 4 L of water through an aspirator. After filtration, the residue was washed with water and dried with hot air, and the α-type crystalline copper phthalocyanine obtained was pulverized. Next, the obtained fine α-type crystal copper phthalocyanine was heated and stirred at 170 ° C. for 6 hours in 1000 parts by weight of sulfolane together with 15 parts by weight of ε-type crystal copper phthalocyanine and 4 parts by weight of iodine. After cooling to near room temperature, it was poured into 1000 parts by weight of methanol, filtered, and the residue was washed with methanol and dried with hot air. Ε-type crystalline copper phthalocyanine containing no α-type or β-type was quantitatively obtained by powder X-ray diffraction analysis. The powder X-ray diffraction profile is shown in FIG. Further, FIG. 4 shows a DTA curve obtained by a differential thermal analysis method at a heating rate of 5 ° C. · min −1 in an air atmosphere. While the exothermic peak in the temperature range of 425 ± 25 ° C. is two in the comparative example, Example 1 is single, and the difference due to the presence or absence of the derivative is clear.

粗製銅フタロシアニン80重量部を500重量部の98%硫酸に加え3時間かき混ぜて硫酸溶液とし4Lの水中にアスピレ−タを通して注入した。濾過後、残渣を水洗、熱風乾燥し、得られたα型結晶形銅フタロシアニンを粉砕した。 次に、得られた微細α型結晶形銅フタロシアニンをε型結晶形銅フタロシアニン20重量部および臭素8重量部
と共に、スルホラン1000重量部中、130℃、10時間加熱撹拌した。室温付近まで冷却後、メタノール1
000重量部中へ注入し、濾過後、残渣をメタノール洗、熱風乾燥した。粉末X線回折分析法でα型およびβ型
を全く含まないε型結晶形銅フタロシアニンが定量的に得られた。
80 parts by weight of crude copper phthalocyanine was added to 500 parts by weight of 98% sulfuric acid and stirred for 3 hours to form a sulfuric acid solution, which was poured into 4 L of water through an aspirator. After filtration, the residue was washed with water and dried with hot air, and the α-type crystalline copper phthalocyanine obtained was pulverized. Next, the obtained fine α-type crystal copper phthalocyanine was stirred with heating at 130 ° C. for 10 hours in 1000 parts by weight of sulfolane together with 20 parts by weight of ε-type crystal copper phthalocyanine and 8 parts by weight of bromine. After cooling to near room temperature, methanol 1
After pouring into 000 parts by weight and filtering, the residue was washed with methanol and dried in hot air. Ε-type crystal copper phthalocyanine containing no α-type or β-type was quantitatively obtained by powder X-ray diffraction analysis.

比較例で得られたε型結晶形銅フタロシアニンの粉末X線回折プロファイルPowder X-ray diffraction profile of ε-type crystalline copper phthalocyanine obtained in Comparative Example 比較例で得られたε型結晶形銅フタロシアニンのDTA曲線DTA curve of ε-type crystalline copper phthalocyanine obtained in Comparative Example 実施例1で得られたε型結晶形銅フタロシアニンの粉末X線回折プロファイルPowder X-ray diffraction profile of ε-type crystalline copper phthalocyanine obtained in Example 1 実施例1で得られたε型結晶形銅フタロシアニンのDTA曲線DTA curve of ε-type crystal copper phthalocyanine obtained in Example 1

Claims (7)

空気雰囲気下、昇温速度5℃・min−1での示差熱分析法による温度範囲425±25℃におけ
る発熱ピークが単一であるε型結晶形銅フタロシアニン。
Ε-type crystal form copper phthalocyanine having a single exothermic peak in a temperature range of 425 ± 25 ° C. by differential thermal analysis at a heating rate of 5 ° C./min −1 in an air atmosphere.
銅フタロシアニンをルイス酸共存下、溶剤中80〜250℃で処理することによって得られる請求項
1記載のε型結晶形銅フタロシアニンの製造法。
The method for producing ε-type crystalline copper phthalocyanine according to claim 1, obtained by treating copper phthalocyanine in a solvent at 80 to 250 ° C in the presence of a Lewis acid.
ルイス酸がヨウ素である請求項2記載の製造法。 The process according to claim 2, wherein the Lewis acid is iodine. ルイス酸が臭素である請求項2記載の製造法。
The process according to claim 2, wherein the Lewis acid is bromine.
ルイス酸がキノン類である請求項2記載の製造法。 The process according to claim 2, wherein the Lewis acid is a quinone. 銅フタロシアニンがα型結晶単独またはε型結晶との混合物である請求項2記載の製造法。 The process according to claim 2, wherein the copper phthalocyanine is an α-type crystal alone or a mixture with an ε-type crystal. 銅フタロシアニンがアシッドペースティング法またはアシッドスラリー法によって得られるα型結晶
単独またはε型結晶との混合物である請求項2記載の製造法。
3. The production method according to claim 2, wherein the copper phthalocyanine is an α-type crystal obtained by an acid pasting method or an acid slurry method, or a mixture with an ε-type crystal.
JP2004091537A 2004-03-26 2004-03-26 ε-type crystal copper phthalocyanine and process for producing the same Withdrawn JP2005272760A (en)

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JP2007332317A (en) * 2006-06-16 2007-12-27 Toyo Ink Mfg Co Ltd ε-type copper phthalocyanine pigment, method for producing the same, and coloring composition using the same
JP2010539309A (en) * 2007-09-18 2010-12-16 ソルヴェイ(ソシエテ アノニム) Production of epsilon copper phthalocyanine with small primary particle size and narrow particle size distribution
JP2011503313A (en) * 2007-11-15 2011-01-27 ソルヴェイ(ソシエテ アノニム) Production of epsilon copper phthalocyanine with small primary particle size and narrow particle size distribution by kneading
WO2011023783A2 (en) 2009-08-27 2011-03-03 Commissariat à l'énergie atomique et aux énergies alternatives Method for preparing silica particles containing a phthalocyanine derivative, said particles, and uses thereof
WO2011098504A1 (en) 2010-02-11 2011-08-18 Commissariat à l'énergie atomique et aux énergies alternatives Stöber method for preparing silica particles containing a phthalocyanine derivative, said particles and the uses thereof
WO2012110554A1 (en) 2011-02-16 2012-08-23 Commissariat à l'énergie atomique et aux énergies alternatives Process for preparing silica particles containing a phthalocyanine derivative by microwave irradiation, said particles and uses thereof
JP2012520914A (en) * 2009-03-18 2012-09-10 ソルヴェイ(ソシエテ アノニム) Process for producing copper phthalocyanine particles exhibiting alpha crystal morphology
JP2013060487A (en) * 2011-09-12 2013-04-04 Dic Corp ε-TYPE COPPER PHTHALOCYANINE PIGMENT AND PIGMENT COMPOSITION FOR COLOR FILTER USING THE SAME
JP2016023222A (en) * 2014-07-18 2016-02-08 Dic株式会社 Pigment composition for coloring plastic

Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007332317A (en) * 2006-06-16 2007-12-27 Toyo Ink Mfg Co Ltd ε-type copper phthalocyanine pigment, method for producing the same, and coloring composition using the same
TWI418597B (en) * 2006-06-16 2013-12-11 Toyo Ink Mfg Co Ε-type copper phthalocyanine pigment, its manufacturing method and coloring composition
JP2010539309A (en) * 2007-09-18 2010-12-16 ソルヴェイ(ソシエテ アノニム) Production of epsilon copper phthalocyanine with small primary particle size and narrow particle size distribution
JP2011503313A (en) * 2007-11-15 2011-01-27 ソルヴェイ(ソシエテ アノニム) Production of epsilon copper phthalocyanine with small primary particle size and narrow particle size distribution by kneading
JP2012520914A (en) * 2009-03-18 2012-09-10 ソルヴェイ(ソシエテ アノニム) Process for producing copper phthalocyanine particles exhibiting alpha crystal morphology
JP2015143368A (en) * 2009-03-18 2015-08-06 ソルヴェイ(ソシエテ アノニム) METHOD FOR MANUFACTURING COPPER PHTHALOCYANINE (CuPc) PARTICLE EXHIBITING EPSILON CRYSTALLINE FORM
WO2011023783A2 (en) 2009-08-27 2011-03-03 Commissariat à l'énergie atomique et aux énergies alternatives Method for preparing silica particles containing a phthalocyanine derivative, said particles, and uses thereof
WO2011098504A1 (en) 2010-02-11 2011-08-18 Commissariat à l'énergie atomique et aux énergies alternatives Stöber method for preparing silica particles containing a phthalocyanine derivative, said particles and the uses thereof
WO2012110554A1 (en) 2011-02-16 2012-08-23 Commissariat à l'énergie atomique et aux énergies alternatives Process for preparing silica particles containing a phthalocyanine derivative by microwave irradiation, said particles and uses thereof
JP2013060487A (en) * 2011-09-12 2013-04-04 Dic Corp ε-TYPE COPPER PHTHALOCYANINE PIGMENT AND PIGMENT COMPOSITION FOR COLOR FILTER USING THE SAME
JP2016023222A (en) * 2014-07-18 2016-02-08 Dic株式会社 Pigment composition for coloring plastic

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